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利用富含氨的废水衍生吸收剂通过化学吸收进行沼气升级。

Biogas upgrading by chemical absorption using ammonia rich absorbents derived from wastewater.

机构信息

Cranfield Water Science Institute, Building 39, Cranfield University, Bedfordshire, MK43 0AL, UK.

Cranfield Water Science Institute, Building 39, Cranfield University, Bedfordshire, MK43 0AL, UK.

出版信息

Water Res. 2014 Dec 15;67:175-86. doi: 10.1016/j.watres.2014.09.010. Epub 2014 Sep 18.

DOI:10.1016/j.watres.2014.09.010
PMID:25277752
Abstract

The use of ammonia (NH3) rich wastewaters as an ecological chemical absorption solvent for the selective extraction of carbon dioxide (CO2) during biogas upgrading to 'biomethane' has been studied. Aqueous ammonia absorbents of up to 10,000 gNH3 m(-3) demonstrated CO2 absorption rates higher than recorded in the literature for packed columns using 20,000-80,000 g NH3 m(-3) which can be ascribed to the process intensification provided by the hollow fibre membrane contactor used in this study to support absorption. Centrifuge return liquors (2325 g m(-3) ionised ammonium, NH4(+)) and a regenerant (477 gNH4(+) m(-3)) produced from a cationic ion exchanger used to harvest NH4(+) from crude wastewater were also tested. Carbon dioxide fluxes measured for both wastewaters compared reasonably with analogue ammonia absorption solvents of equivalent NH3 concentration. Importantly, this demonstrates that ammonia rich wastewaters can facilitate chemically enhanced CO2 separation which eliminates the need for costly exogenic chemicals or complex chemical handling which are critical barriers to implementation of chemical absorption. When testing NH3 analogues, the potential to recover the reaction product ammonium bicarbonate (NH4HCO3) in crystalline form was also illustrated. This is significant as it suggests a new pathway for ammonia separation which avoids biological nitrification and produces ammonia stabilised into a commercially viable fertiliser (NH4HCO3). However, in real ammonia rich wastewaters, sodium bicarbonate and calcium carbonate were preferentially formed over NH4HCO3 although it is proposed that NH4HCO3 can be preferentially formed by manipulating both ion exchange and absorbent chemistry.

摘要

已研究使用富含氨(NH3)的废水作为生态化学吸收溶剂,用于从沼气升级为“生物甲烷”过程中选择性提取二氧化碳(CO2)。含有高达 10000 gNH3 m(-3) 的氨水溶液吸收剂表现出的 CO2 吸收速率高于使用 20000-80000 g NH3 m(-3) 的填充柱在文献中记录的值,这可归因于本研究中使用的中空纤维膜接触器为吸收提供的过程强化。还测试了从用于从粗废水回收 NH4(+)的阳离子离子交换器产生的离心机回流水(2325 g m(-3) 离子化的铵,NH4(+))和再生剂(477 gNH4(+) m(-3))。两种废水的 CO2 通量与具有等效 NH3 浓度的模拟氨吸收溶剂相当。重要的是,这表明富含氨的废水可以促进化学增强的 CO2 分离,从而消除了对昂贵的外源性化学物质或复杂化学处理的需求,这是化学吸收实施的关键障碍。在测试 NH3 类似物时,还说明了以结晶形式回收反应产物碳酸氢铵(NH4HCO3)的潜力。这很重要,因为它表明了一种新的氨分离途径,避免了生物硝化作用,并产生了氨稳定为商业上可行的肥料(NH4HCO3)。然而,在实际的富含氨的废水中,优先形成了碳酸氢钠和碳酸钙,而不是 NH4HCO3,尽管据提议可以通过操纵离子交换和吸收剂化学来优先形成 NH4HCO3。

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